Method for preparing zeolite molecular sieve by using oil shale residues
A technology of oil shale waste residue and zeolite molecular sieve, which is applied to the removal of solid waste and crystalline aluminosilicate zeolite, etc., can solve the problems of pollution, occupation of land and environment, avoid large accumulation, reduce environmental pollution, and improve utilization rate Effect
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Embodiment 1
[0017] ①Take 100 g of oil shale waste residue that has been ground to below 100 mesh and roasted and activated at 550°C for 2 hours;
[0018] ② To the roasted waste residue, add H with a mass concentration of 30% according to a mass ratio of 1:3. 2 SO 4 Solution, heated to 90-95 ° C for 5 hours, hot filtered, separated into a primary aluminum-iron solution and filter residue, washed the resulting filter residue with water 1-2 times, and the obtained washing solution was incorporated into the primary aluminum-iron solution;
[0019] 3. Evaporate the primary aluminum-iron solution obtained in step 2. to 2 / 6 of the original volume, cool and crystallize, filter to obtain aluminum sulfate crystals and acid-containing aluminum-iron filtrate;
[0020] ④ According to the mass ratio of 1:3, the acid-containing aluminum-iron filtrate obtained in step ③ is mixed with the newly added oil shale waste residue, heated to 90-95 ° C for 3 hours, cooled and crystallized, filtered to obtain alu...
Embodiment 2
[0026] ①Take 200g of oil shale waste residue that has been ground to below 100 mesh and activated at 550°C for 2 hours;
[0027] ② To the roasted waste residue, add H with a mass concentration of 30% according to a mass ratio of 1:3. 2 SO 4 Solution, heated to 90-95 ° C for 5 hours, hot filtered, separated into a primary aluminum-iron solution and filter residue, washed the resulting filter residue with water 1-2 times, and the obtained washing solution was incorporated into the primary aluminum-iron solution;
[0028] 3. the primary aluminum-iron solution obtained in step 2. is evaporated to 4 / 6 of the original volume, crystallized by cooling, and filtered to obtain aluminum sulfate crystals and acid-containing aluminum-iron filtrate;
[0029] ④ According to the mass ratio of 1:3, the acid-containing aluminum-iron filtrate obtained in the previous step ③ is mixed with the newly added oil shale waste residue, heated to 90-95 ° C for 3 hours, cooled and crystallized, filtered ...
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